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Process for the reduction of NH/sub 3/ in regeneration zone off gas by select recycle of certain-sized NH/sub 3/ decomposition catalysts

Patent ·
OSTI ID:6549191

This patent describes a process for the fluidized catalytic cracking of a higher molecular weight hydrocarbon to a lower molecular weight hydrocarbon which process comprises: (a) contacting, in a cracking zone, the higher molecular weight hydrocarbon with a cracking catalyst, wherein the cracking catalyst becomes deactivated with coke deposits while being employed in the cracking; (b) withdrawing deactivated cracking catalyst particles from the cracking zone having the coke deposited thereon and passing the coked catalyst to a regeneration zone containing an ammonia decomposition catalyst and an inlet means for admission to the regeneration zone of a sufficient quantity of an oxygen-containing gas to operate the regeneration zone of partial combustion as defined by the presence of from 1 to 6 volume percent of CO in the regeneration zone; (c) containing the coke-deposited cracking catalyst with the oxygen-containing gas in the presence of the ammonia decomposition catalyst comprising a noble metal dispersed on an alumina support to form a regeneration zone effluent stream comprising spent regeneration gas, regenerated catalyst, and ammonia decomposition catalyst; (d) withdrawing the regeneration zone effluent stream from the regeneration zone and passing the regeneration zone effluent stream to a separation means wherein the spent regeneration gas, regenerated catalyst and ammonia decomposition catalyst are separated and wherein the spent regeneration gas is passed to a CO combustion zone.

Assignee:
Shell Oil Co., Houston, TX
Patent Number(s):
US 4755282
OSTI ID:
6549191
Country of Publication:
United States
Language:
English